US20230221082A1 - Heat exchanger with undulating parting sheets - Google Patents

Heat exchanger with undulating parting sheets Download PDF

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Publication number
US20230221082A1
US20230221082A1 US18/059,980 US202218059980A US2023221082A1 US 20230221082 A1 US20230221082 A1 US 20230221082A1 US 202218059980 A US202218059980 A US 202218059980A US 2023221082 A1 US2023221082 A1 US 2023221082A1
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US
United States
Prior art keywords
layer
sheet
plane
lower sheet
heat exchanger
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Pending
Application number
US18/059,980
Inventor
Tomasz Meczkowski
Hubert Siudzinski
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Hamilton Sundstrand Corp
Original Assignee
Utc Aerospace Systems Wroclow Sp Z OO
Hamilton Sundstrand Corp
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Application filed by Utc Aerospace Systems Wroclow Sp Z OO, Hamilton Sundstrand Corp filed Critical Utc Aerospace Systems Wroclow Sp Z OO
Assigned to HAMILTON SUNDSTRAND CORPORATION reassignment HAMILTON SUNDSTRAND CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: UTC AEROSPACE SYSTEMS WROCLAW SP. Z O.O.
Assigned to UTC AEROSPACE SYSTEMS WROCLOW SP. Z O.O. reassignment UTC AEROSPACE SYSTEMS WROCLOW SP. Z O.O. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: Meczkowski, Tomasz, Siudzinski, Hubert
Publication of US20230221082A1 publication Critical patent/US20230221082A1/en
Pending legal-status Critical Current

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F7/00Elements not covered by group F28F1/00, F28F3/00 or F28F5/00
    • F28F7/02Blocks traversed by passages for heat-exchange media
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/025Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being corrugated, plate-like elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B33ADDITIVE MANUFACTURING TECHNOLOGY
    • B33YADDITIVE MANUFACTURING, i.e. MANUFACTURING OF THREE-DIMENSIONAL [3-D] OBJECTS BY ADDITIVE DEPOSITION, ADDITIVE AGGLOMERATION OR ADDITIVE LAYERING, e.g. BY 3-D PRINTING, STEREOLITHOGRAPHY OR SELECTIVE LASER SINTERING
    • B33Y80/00Products made by additive manufacturing
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/022Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being wires or pins
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/03Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/03Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits
    • F28D1/0308Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other
    • F28D1/035Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other with U-flow or serpentine-flow inside the conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/03Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits
    • F28D1/0366Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by spaced plates with inserted elements
    • F28D1/0383Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by spaced plates with inserted elements with U-flow or serpentine-flow inside the conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0031Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
    • F28D9/0043Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
    • F28D9/0056Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another with U-flow or serpentine-flow inside conduits; with centrally arranged openings on the plates
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0062Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements
    • F28D9/0068Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements with means for changing flow direction of one heat exchange medium, e.g. using deflecting zones
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0093Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/08Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by varying the cross-section of the flow channels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2250/00Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
    • F28F2250/02Streamline-shaped elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
    • F28F3/042Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
    • F28F3/048Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of ribs integral with the element or local variations in thickness of the element, e.g. grooves, microchannels
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Definitions

  • the present disclosure relates to a layer for a heat exchanger, a heat exchanger, and a method of making a layer for a heat exchanger.
  • Heat exchanger designs have a flowpath defined between an inlet of the heat exchanger and an outlet of the heat exchanger, and between upper and lower plates that extend between the inlet and outlet. Heat exchange to or from a fluid flowing in the flowpath occurs primarily through the upper and lower plates. It is known to provide pins that extend in the flowpath, between the upper and lower plates, to improve the heat transfer.
  • a layer for a heat exchanger comprising: an inlet; an outlet; an upper sheet; a lower sheet; a fluid flowpath defined between the upper sheet and lower sheet and from the inlet to the outlet; and at least one pin disposed in the flowpath and connecting the upper sheet to the lower sheet; wherein the lower sheet has a first undulating profile; and wherein the upper sheet has a second undulating profile different from the first undulating profile.
  • Defining a fluid flowpath between upper and lower sheets with different undulating profiles greatly increases the turbulence of the fluid flow in the flowpath.
  • the heat transfer of the heat exchanger layer is increased.
  • undulating sheets have an increased primary heat transfer area compared to conventional/straight parting sheets.
  • Each undulating profile may comprise at least one of: undulations extending along a first axis; and undulations extending along a second axis; wherein the first axis and the second axis are non-parallel.
  • the second axis may be oriented at an angle between 0 degrees and 180 degrees from the first axis.
  • the second axis may be perpendicular to (i.e. oriented at 90 degrees from) the first axis.
  • the second axis may be skewed from the first axis.
  • the first undulating profile may comprise undulations extending along the first axis and having a first undulation wavelength; and the second undulating profile may comprise undulations extending along the first axis and having a second undulation wavelength different to the first undulation wavelength.
  • the undulation wavelengths extending along the first and second axes may be the same.
  • the first undulating profile may comprise undulations extending along the first axis and having a first phase of undulation; and the second undulating profile may comprise undulations extending along the first axis and having a second phase of undulation different to the first phase of undulation.
  • the first undulating profile may comprise undulations extending along the first axis; and the second undulating profile may comprise undulations extending along the first axis; wherein the undulations of the second undulating profile are offset from the undulations of the first undulating profile.
  • the layer may comprise a plurality of pins disposed in the flowpath, each pin connecting between the upper sheet and lower sheet and having a pin height defined between the upper and lower sheet, wherein at least two of the plurality of pins have different pin heights.
  • At least one of the upper sheet and the lower sheet may be formed from an aluminium alloy, a titanium alloy, or an austenitic nickel-chromium-based superalloy.
  • a heat exchanger comprising a first layer and a second layer; wherein the first layer is a layer according to the preceding aspect; wherein the second layer is a layer according to the preceding aspect; and wherein the upper sheet of the second layer is also the lower sheet of the first layer.
  • the upper sheet of the first layer may extend along a first plane and the lower sheet of the first layer may extend along a second plane.
  • the plane may be defined as the plane that bisects the undulating profile, along the direction of the undulations.
  • the first plane and the second plane may be non-parallel.
  • the first plane may be oriented at an angle between 1 and 10 degrees from the second plane.
  • the first plane may be at an angle between 1 and 5 degrees from the second plane.
  • the first plane and the second plane may be parallel.
  • the lower sheet of the second layer may extend along a third plane.
  • the first layer may have a first section undulating around the first plane in a first section of the first layer, and may have a second section wherein the undulations undulate around a different plane. That is, the different plane of the second section may be non-co-planar with the first plane of the first section.
  • the average distance between the upper and lower sheets of the first layer may be different from the average distance between the upper and lower sheets of the second layer. Put another way, the first layer may have a different average height from the second layer.
  • the number of pins disposed in the flowpath of the first layer may be different from the number of pins disposed in the flowpath of the second layer.
  • a pin pattern of the pin(s) disposed in the flowpath of the first layer may be different from a pin pattern of the pin(s) disposed in the flowpath of the second layer.
  • a method of additively manufacturing a layer for a heat exchanger comprising: additively manufacturing a lower sheet having a first undulating profile; additively manufacturing at least one pin on the lower sheet; and providing an upper sheet on top of the pin, the upper sheet having a second undulating profile different from the first undulating profile.
  • additive manufacturing may help in the construction of the undulating profile of the lower sheet and/or the upper sheet. Furthermore, construction of the or each pin directly onto a lower sheet with an undulating profile is made easier using additive manufacturing, and the accuracy of placement and orientation of the pins on the undulating profile of the lower sheet may be improved compared to traditional (non-additive) manufacturing methods.
  • the method may comprise additively manufacturing a plurality of pins on the lower sheet, wherein at least two of the plurality of pins have a different pin height.
  • the method may comprise additively manufacturing a sidewall extending between the lower sheet and the upper sheet; and optionally additively manufacturing one or more sets of turning vanes on the lower sheet at the same time as additively manufacturing the or each pin.
  • Additively manufacturing the sidewall may be simpler than using traditional manufacturing techniques.
  • Turning vanes may be desirable in layers having a non-straight flow path, e.g. a U-shaped flow path, and additively manufacturing these may be simpler than using traditional (non-additive) manufacturing techniques.
  • a method of additively manufacturing a heat exchanger comprising: additively manufacturing a first plurality of layers interleaved with a second plurality of layers, wherein each layer of the first and second pluralities of layers is manufactured via the method of the preceding aspect; additively manufacturing a first header fluidly connected to each of the first plurality of layers; and additively manufacturing a second header fluidly connected to each of the second plurality of layers.
  • Each step of additive manufacturing may be performed using a metal powder bed SLM additive manufacturing process.
  • a powder of the metal powder bed may be one of an aluminium alloy, a titanium alloy, and an austenitic nickel-chromium-based superalloy.
  • SLM is a relatively mature additive-manufacturing technology and typically allows recovery of unused (i.e. unmelted) powder from the finished article.
  • the unused powder may be used in future additive-manufacturing operations and thus this method may be cost effective by minimizing wastage of (potentially expensive) metal powder.
  • the heat exchanger constructed in accordance with this aspect may have a compact design allowing for good heat exchange between fluids flowing in their respective pluralities of layers.
  • FIG. 1 shows a perspective view of a heat exchanger
  • FIG. 2 shows a plan view of a layer within the heat exchanger
  • FIG. 3 shows a perspective view of undulated sheets for use in the heat exchanger
  • FIG. 4 shows a perspective view of a fluid flowpath of the undulated sheets of FIG. 3 ;
  • FIG. 5 shows a side view of two layers formed by three undulated sheets within the heat exchanger
  • FIG. 6 shows a side view of an example layer within a heat exchanger wherein the upper and lower sheets are non-parallel
  • FIG. 7 shows a method of making a heat exchanger.
  • FIG. 1 shows a heat exchanger 10 having a heat exchanger core 11 , a first header 12 for conveying a first fluid into and out of the core 11 , and a second header 14 for conveying a second fluid into and out of the core 11 .
  • the heat exchanger may be primarily used to exchange heat between the first fluid and the second fluid. However, heat may also be exchanged out through the sidewall 40 as well as out of the top and bottom sides of the heat exchanger core 11 .
  • the first header 12 connects to a first plurality of layers 30 a,c,e , . . . 30 n of the heat exchanger core 11 .
  • the second header 14 connects to a second plurality of layers 30 b,d , . . . 30 n ⁇ 1 of the heat exchanger core 11 .
  • the first plurality of layers 30 a,c,e . . . 30 n is interleaved with the second plurality of layers 30 b,d . . . 30 n ⁇ 1 such that for example, layer 30 b is located between layers 30 a and 30 c .
  • 30 n is fluidly isolated from the second fluid flowing in the second plurality of layers 30 b,d . . . 30 n ⁇ 1.
  • These layers may be generically referred to by reference numeral 30 and any layer of the first and second pluralities of layers may be a layer 30 as shown in FIG. 2 .
  • the layer 30 comprises an inlet 32 and an outlet 34 , a sidewall 40 , and (with brief reference to FIG. 5 ) an upper sheet 36 , and a lower sheet 38 .
  • fluid is constrained by the upper sheet 36 , lower sheet 38 , and sidewall 40 , so as to flow from the inlet 32 , through the layer 30 , to the outlet 34 . That is, the upper sheet 36 , lower sheet 38 , and sidewall 40 together define a flowpath for fluid flowing in the layer 30 .
  • the layer 30 shown in FIG. 2 defines a generally U-shaped flowpath between the inlet 32 and outlet 34 .
  • the upper sheet 36 of a given layer e.g. layer 30 b
  • a first portion of the first header 12 connects to the inlet side 30 of each layer 30 a,c,e . . . n of the first plurality of layers, and, in use, fluid is pumped into the first portion and flows into the inlet side 32 of every layer connected to the first header 12 .
  • the fluid flows through each of the layers 30 a,c,e . . . n and out through the outlet 34 of each layer 30 a,c,e . . . n of the first plurality of layers.
  • the outlets 34 are all connected to a second portion of the first header 12 , the second portion being fluidly isolated from the first portion. Fluid flows into the second portion and then out of the first header 12 .
  • a first portion of the second header 14 connects to the inlet side 30 of each layer 30 b,d . . . n ⁇ 1 and, in use, fluid is pumped into the first portion and flows into the inlet side 32 of every layer connected to the second header 14 .
  • the fluid flows through each of the layers 30 a,c,e , . . . n and out through the outlet 34 of each layer.
  • the outlets 34 are all connected to the second portion of the second header 14 , the second portion being fluidly isolated from the first portion. Fluid flows into the second portion and then out of the second header 14 .
  • each layer 30 as shown in FIG. 2 , one or more pins 100 are disposed in the fluid flowpath. Each pin 100 extends between the lower sheet 38 and the upper sheet 36 .
  • each layer 30 there may be provided within each layer 30 a first set of turning vanes 42 a that may turn the flow through 90 degrees, and a second set of turning vanes 42 b that may turn the flow through a further 90 degrees, to create the overall U-shaped flow path.
  • a plurality of pins 100 may be disposed between the first and second sets of turning vanes 42 a,b .
  • the pins 100 shown in FIG. 2 are all arranged within the layer 30 such that each pin 100 faces directly into a local flow direction.
  • FIG. 3 shows three sheets 301 , 302 , 303 (each of which may act as an upper or a lower sheet of a layer 30 ), each sheet having a different undulating profile.
  • FIG. 4 shows sheets 301 , 302 , 303 with some exemplary fluid flowpaths that fluid may take when moving across the sheet.
  • Sheet 301 has an undulating profile comprising undulations extending along a first axis X.
  • Sheet 302 has an undulating profile comprising undulations extending along a second axis Y which is non-parallel with the first axis X.
  • the second axis Y is perpendicular to the first axis X, i.e. the second axis Y is oriented at 90 degrees from the first axis X.
  • the second axis Y may be oriented at any angle between 0 degrees and 180 degrees from the first axis, e.g. at 30 degrees or at 45 degrees.
  • the second axis Y is different from the first axis X, and may be 90 degrees to the first axis X or skew to the first axis X.
  • the first axis X lies in the plane of sheet 301 and the second axis Y lies in the plane of sheet 302 .
  • Sheet 303 has an undulating profile comprising undulations extending along the first axis X and undulations extending along the second axis Y.
  • the second axis Y is shown as perpendicular to the first axis X.
  • second axis Y may extend at a different angle (i.e. not 90 degrees) to the first axis X.
  • the first axis X and second axis Y lie in the plane of sheet 303 .
  • sheet 301 forms one of the upper or lower sheet of the layer
  • sheet 302 forms the other of the upper or lower sheet of the layer.
  • the flowpath defined between these sheets 301 , 302 causes increased turbulence of the fluid flowing through it, and thus increases the mixing of fluid particles.
  • the heat transfer coefficient of the layer is increased, thus improving the efficiency of the heat exchanger.
  • a layer 30 comprises sheet 303 as an upper (or lower) sheet and comprise sheet 301 or sheet 302 as the corresponding lower (or upper) sheet.
  • the undulating profile of sheet 303 comprises an additional set of undulations compared to the undulating profile of sheet 301 or sheet 302 which extends along a different axis (i.e. non-parallel) to the axis of the undulations of sheet 301 or sheet 302 , and such an arrangement of sheets thus increases the turbulence of the fluid flowing between.
  • Exemplary fluid paths, which are dictated by the undulating profiles of each of sheet 301 , sheet 302 , and sheet 303 are shown in FIG. 4 .
  • FIG. 5 shows a side view of a first layer 30 a and a second layer 30 b in the heat exchanger 10 .
  • lower sheet 38 a of the first layer 30 a has an undulating profile comprising undulations extending at least along a first axis X
  • upper sheet 36 a of the first layer 30 a also has an undulating profile comprising undulations extending at least along a first axis X.
  • the undulations of each sheet comprise a sequence of alternating peaks and troughs.
  • the undulations may be sinusoidal.
  • the undulations may have a wavelength and a phase.
  • the wavelength of the undulations may be constant, e.g. a distance between each consecutive peak of the undulations is constant.
  • the undulations of the lower sheet 38 a have a first wavelength w 1 that is longer than a second wavelength w 2 of the undulations of the upper sheet 36 a .
  • a first distance between the peaks of the undulations of the lower sheet 38 a may be greater than a second distance between the peaks of the undulations of the upper sheet 36 a.
  • a first phase ⁇ 1 of the undulations of the lower sheet 38 a is different from a second phase ⁇ 2 of the undulations of the upper sheet 36 a .
  • the undulations of the lower sheet 38 a are offset from the undulations of the upper sheet 36 a to promote turbulent flow in the heat exchanger layer 30 a.
  • the lower sheet 38 a of the first layer 30 a may simultaneously function as an upper sheet 36 b of a second layer 30 b , and in that case the undulating profile of the upper sheet 36 b of layer 30 b is also the undulating profile of the lower sheet 38 a of layer 30 a.
  • the upper sheet 36 a of layer 30 a which has an undulating profile different to that of the lower sheet 38 a , may have an undulating profile the same as that of the lower sheet 38 b of layer 30 a (e.g. so the undulating profiles of the sheets in the heat exchanger alternate).
  • the undulating profiles of the sheets may be randomly ordered (or ordered in some other manner) provided the undulating profiles of adjacent sheets (i.e. sheets that together form a single layer 30 ) are different from one another.
  • the undulations of the lower sheet 38 b that are extending along a first axis X have a third wavelength w 3 that is different to the first wavelength w 1 but the same as the second wavelength w 2 , and a third phase ⁇ 3 that is different to the first phase ⁇ 1 and the second phase ⁇ 2 .
  • the sheets of the first layer 30 a and second layer 30 b may or may not have undulations extending along the second axis Y, but these are not visible in FIG. 5 .
  • the pins 100 in the layer 30 a are arranged in a pin pattern adapted to suit the requirements of the layer 30 a , e.g. considering the undulating profile of the upper sheet 36 a and the undulating profile of the lower sheet 38 a .
  • Each pin 100 extends between the upper and lower sheet, defining a pin height h p .
  • the pin height of each pin is dependent on the positioning of the pins 100 (e.g. the pin pattern) relative to the undulating profiles of the upper sheet and the lower sheet. As such, at least two of the plurality of pins may have different pin heights.
  • a short pin may have a height h p 1 and be positioned at or near to a peak of an undulation of the lower sheet 38 a and connected to the upper sheet 36 at or near to a trough of an undulation of the upper sheet 36 a .
  • a long pin may have a height h p 2 and be positioned at or near to a trough of the lower sheet 38 a so that it may be connected to the upper sheet 36 b at or near a peak of an undulation of the upper sheet 36 a .
  • the long pin having height h p 2 is longer than the short pin having a height h p 1 .
  • the first layer 30 a may have a different number of pins and/or a different pin pattern from the second layer 30 b.
  • each sheet is generally planar in shape, e.g. each sheet generally extends along a plane XY, and the undulations are variations in the “z” direction.
  • a lower sheet 38 extends along a first plane p 1 and an upper sheet 36 extends along a second plane p 2 .
  • the first plane p 1 and the second plane p 2 are disposed apart from each other so the upper sheet 36 and lower sheet 38 define the flowpath therebetween.
  • the plane may be defined as the plane that bisects the undulating profile along the direction of undulations of a given sheet.
  • the first plane p 1 and the second plane p 2 may be parallel (and a third plane p 3 of the lower sheet 38 b of the second layer 30 b may also be parallel with the first plane p 1 and the second plane p 2 ).
  • the layer 30 a has a constant average height (note, due to the upper and lower sheets having different undulations e.g. in terms of phase, undulation-direction etc., the height at one point within the layer will differ from the height in another location within that layer).
  • An average height of each layer of the first plurality of layers 30 a,c,e . . . 30 n may be different from an average height of each layer of the second plurality of layers 30 b,d . . . 30 n ⁇ 1. This may have particular advantages where the first fluid is different from the second fluid.
  • the first plane p 1 and the second plane p 2 are non-parallel.
  • the first plane p 1 may be oriented at an angle ⁇ between 0 and 10 degrees (e.g. 0° ⁇ 10°) from the second plane p 2 along the X axis, as shown in FIG. 6 . In one example, 5° ⁇ 10°.
  • the first plane p 1 and the second plane p 2 may be oriented at an angle ⁇ between 0 and 10 degrees (e.g. 0° ⁇ 10°) from the second plane p 2 along the Y axis (not shown). In one example, 5° ⁇ 10°. Angling the upper sheet 36 and lower sheet 38 relative to each other may further increase turbulence of the fluid flow in the layer 30 .
  • Each sheet may have a first section undulating around the first plane in a first section of the first layer, and may have a second section wherein the undulations undulate around a different plane. That is, the different plane may be non-co-planar with the first plane of the first section.
  • Each layer 30 may be produced by additive manufacturing, such as by the process shown in FIG. 7 .
  • a lower sheet 38 is additively manufactured, the lower sheet 38 having a first undulating profile (step 502 ).
  • pins 100 are additively manufactured on the lower sheet 38 .
  • an upper sheet 36 is provided on top of the pins 100 , the upper sheet 36 having a second undulating profile different from the first undulating profile.
  • the process may optionally include additively manufacturing one or more of: the sidewall 40 , turning vanes 42 a,b , further layers 30 on top of the initially formed layer 30 , and one or more headers connecting to each layer 30 .
  • Each layer 30 may be produced by a SLM powder-bed method of additive manufacturing.
  • a first layer of metal powder is provided and a portion of the powder is melted by a laser beam to “print” the first layer of the overall object.
  • the first layer is then lowered and a second layer of powder is brushed over the first layer, and a portion of the second layer of powder is melted by the laser beam to print a second layer of the overall object.
  • a three-dimensional object is built-up layer-by-layer and, once all layers of the object have been printed, the loose (i.e. unmelted) powder is removed to reveal the object.
  • the upper sheet 36 may be a pre-existing (e.g. manufactured by a previous additive manufacturing process) layer that is connected to the top of the pins 100 after construction of the pins 100 on the lower sheet 38 .
  • the upper sheet 38 may be additively manufactured after the pins 100 have been manufactured, by continuing the additive manufacturing process.
  • a new layer 30 (e.g. layer 30 n ⁇ 1) may be formed directly on top of the first layer 30 .
  • the upper sheet 36 of the first layer 30 becomes the bottom sheet 38 of the new layer 30 . That is, the same layer of material may simultaneously function as the upper sheet 36 of one layer 30 , and the bottom sheet 38 of another layer 30 .
  • the sidewall 40 may have an undulating cross-section, e.g. as shown in FIGS. 1 and 2 . This may increase the heat transfer across the sidewall 40 and/or may increase the strength of the sidewall for a given wall thickness.
  • any or all parts of the heat exchanger 10 may be made from metal.
  • some or all parts are made from an austenitic nickel-chromium-based superalloy, such as the Iconel family of metals manufactured by the Special Metals Corporation of New York state, USA.
  • some or all parts may be made from an aluminium alloy or a titanium alloy.
  • the first and second fluids may be oil, such that the heat exchanger 10 is an oil-oil heat exchanger.
  • the first fluid may be different from the second fluid.
  • Other fluids, including air, water, fuel(s), or carbon dioxide are also envisaged for either or both of the first and second fluids.

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Abstract

A layer for a heat exchanger includes: an inlet; an outlet; an upper sheet; a lower sheet; a fluid flowpath defined between the upper sheet and lower sheet and from the inlet to the outlet; and at least one pin disposed in the flowpath and connecting the upper sheet to the lower sheet; wherein the lower sheet has a first undulating profile. The upper sheet has a second undulating profile different from the first undulating profile. Also disclosed is a heat exchanger including the layer, and a method of making a layer for a heat exchanger.

Description

    CROSS-REFERENCE TO RELATED APPLICATION
  • This application claims the benefit of European Patent Application No. 22461501.3 filed on Jan. 8, 2022, the whole disclosure of which is incorporated herein by reference.
  • BACKGROUND
  • The present disclosure relates to a layer for a heat exchanger, a heat exchanger, and a method of making a layer for a heat exchanger.
  • Many heat exchanger designs have a flowpath defined between an inlet of the heat exchanger and an outlet of the heat exchanger, and between upper and lower plates that extend between the inlet and outlet. Heat exchange to or from a fluid flowing in the flowpath occurs primarily through the upper and lower plates. It is known to provide pins that extend in the flowpath, between the upper and lower plates, to improve the heat transfer.
  • Such conventional heat exchangers have generally been considered satisfactory for their intended purpose but there is a need in the art for improved heat exchangers.
  • SUMMARY
  • According to a first aspect, there is provided a layer for a heat exchanger, the layer comprising: an inlet; an outlet; an upper sheet; a lower sheet; a fluid flowpath defined between the upper sheet and lower sheet and from the inlet to the outlet; and at least one pin disposed in the flowpath and connecting the upper sheet to the lower sheet; wherein the lower sheet has a first undulating profile; and wherein the upper sheet has a second undulating profile different from the first undulating profile.
  • Defining a fluid flowpath between upper and lower sheets with different undulating profiles greatly increases the turbulence of the fluid flow in the flowpath. By increasing the turbulence of the fluid flow, the heat transfer of the heat exchanger layer is increased. Furthermore, undulating sheets have an increased primary heat transfer area compared to conventional/straight parting sheets.
  • Each undulating profile may comprise at least one of: undulations extending along a first axis; and undulations extending along a second axis; wherein the first axis and the second axis are non-parallel.
  • In other words, the second axis may be oriented at an angle between 0 degrees and 180 degrees from the first axis. For example, the second axis may be perpendicular to (i.e. oriented at 90 degrees from) the first axis. In another example, the second axis may be skewed from the first axis.
  • The first undulating profile may comprise undulations extending along the first axis and having a first undulation wavelength; and the second undulating profile may comprise undulations extending along the first axis and having a second undulation wavelength different to the first undulation wavelength. Alternatively, the undulation wavelengths extending along the first and second axes may be the same.
  • The first undulating profile may comprise undulations extending along the first axis and having a first phase of undulation; and the second undulating profile may comprise undulations extending along the first axis and having a second phase of undulation different to the first phase of undulation.
  • The first undulating profile may comprise undulations extending along the first axis; and the second undulating profile may comprise undulations extending along the first axis; wherein the undulations of the second undulating profile are offset from the undulations of the first undulating profile.
  • The layer may comprise a plurality of pins disposed in the flowpath, each pin connecting between the upper sheet and lower sheet and having a pin height defined between the upper and lower sheet, wherein at least two of the plurality of pins have different pin heights.
  • At least one of the upper sheet and the lower sheet may be formed from an aluminium alloy, a titanium alloy, or an austenitic nickel-chromium-based superalloy.
  • According to another aspect, there is provided a heat exchanger comprising a first layer and a second layer; wherein the first layer is a layer according to the preceding aspect; wherein the second layer is a layer according to the preceding aspect; and wherein the upper sheet of the second layer is also the lower sheet of the first layer.
  • The upper sheet of the first layer may extend along a first plane and the lower sheet of the first layer may extend along a second plane. The plane may be defined as the plane that bisects the undulating profile, along the direction of the undulations.
  • The first plane and the second plane may be non-parallel.
  • In one example, the first plane may be oriented at an angle between 1 and 10 degrees from the second plane. For example, the first plane may be at an angle between 1 and 5 degrees from the second plane.
  • The first plane and the second plane may be parallel.
  • The lower sheet of the second layer may extend along a third plane.
  • The first layer may have a first section undulating around the first plane in a first section of the first layer, and may have a second section wherein the undulations undulate around a different plane. That is, the different plane of the second section may be non-co-planar with the first plane of the first section.
  • The average distance between the upper and lower sheets of the first layer may be different from the average distance between the upper and lower sheets of the second layer. Put another way, the first layer may have a different average height from the second layer. The number of pins disposed in the flowpath of the first layer may be different from the number of pins disposed in the flowpath of the second layer.
  • A pin pattern of the pin(s) disposed in the flowpath of the first layer may be different from a pin pattern of the pin(s) disposed in the flowpath of the second layer.
  • According to another aspect, there is provided a method of additively manufacturing a layer for a heat exchanger, the method comprising: additively manufacturing a lower sheet having a first undulating profile; additively manufacturing at least one pin on the lower sheet; and providing an upper sheet on top of the pin, the upper sheet having a second undulating profile different from the first undulating profile.
  • Using additive manufacturing may help in the construction of the undulating profile of the lower sheet and/or the upper sheet. Furthermore, construction of the or each pin directly onto a lower sheet with an undulating profile is made easier using additive manufacturing, and the accuracy of placement and orientation of the pins on the undulating profile of the lower sheet may be improved compared to traditional (non-additive) manufacturing methods.
  • The method may comprise additively manufacturing a plurality of pins on the lower sheet, wherein at least two of the plurality of pins have a different pin height.
  • The method may comprise additively manufacturing a sidewall extending between the lower sheet and the upper sheet; and optionally additively manufacturing one or more sets of turning vanes on the lower sheet at the same time as additively manufacturing the or each pin.
  • Additively manufacturing the sidewall may be simpler than using traditional manufacturing techniques. Turning vanes may be desirable in layers having a non-straight flow path, e.g. a U-shaped flow path, and additively manufacturing these may be simpler than using traditional (non-additive) manufacturing techniques.
  • According to another aspect, there is provided a method of additively manufacturing a heat exchanger, the method comprising: additively manufacturing a first plurality of layers interleaved with a second plurality of layers, wherein each layer of the first and second pluralities of layers is manufactured via the method of the preceding aspect; additively manufacturing a first header fluidly connected to each of the first plurality of layers; and additively manufacturing a second header fluidly connected to each of the second plurality of layers.
  • Each step of additive manufacturing may be performed using a metal powder bed SLM additive manufacturing process.
  • A powder of the metal powder bed may be one of an aluminium alloy, a titanium alloy, and an austenitic nickel-chromium-based superalloy.
  • SLM is a relatively mature additive-manufacturing technology and typically allows recovery of unused (i.e. unmelted) powder from the finished article. The unused powder may be used in future additive-manufacturing operations and thus this method may be cost effective by minimizing wastage of (potentially expensive) metal powder.
  • The heat exchanger constructed in accordance with this aspect may have a compact design allowing for good heat exchange between fluids flowing in their respective pluralities of layers.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • Certain embodiments of the present disclosure will now be described in greater detail by way of example only and with reference to the accompanying drawings in which:
  • FIG. 1 shows a perspective view of a heat exchanger;
  • FIG. 2 shows a plan view of a layer within the heat exchanger;
  • FIG. 3 shows a perspective view of undulated sheets for use in the heat exchanger;
  • FIG. 4 shows a perspective view of a fluid flowpath of the undulated sheets of FIG. 3 ;
  • FIG. 5 shows a side view of two layers formed by three undulated sheets within the heat exchanger;
  • FIG. 6 shows a side view of an example layer within a heat exchanger wherein the upper and lower sheets are non-parallel; and
  • FIG. 7 shows a method of making a heat exchanger.
  • DETAILED DESCRIPTION
  • FIG. 1 shows a heat exchanger 10 having a heat exchanger core 11, a first header 12 for conveying a first fluid into and out of the core 11, and a second header 14 for conveying a second fluid into and out of the core 11. The heat exchanger may be primarily used to exchange heat between the first fluid and the second fluid. However, heat may also be exchanged out through the sidewall 40 as well as out of the top and bottom sides of the heat exchanger core 11.
  • The first header 12 connects to a first plurality of layers 30 a,c,e, . . . 30 n of the heat exchanger core 11. The second header 14 connects to a second plurality of layers 30 b,d, . . . 30 n−1 of the heat exchanger core 11. The first plurality of layers 30 a,c,e . . . 30 n is interleaved with the second plurality of layers 30 b,d . . . 30 n−1 such that for example, layer 30 b is located between layers 30 a and 30 c. At least within the heat exchanger 10, the first fluid flowing in the first plurality of layers 30 a,c,e . . . 30 n is fluidly isolated from the second fluid flowing in the second plurality of layers 30 b,d . . . 30 n−1. These layers may be generically referred to by reference numeral 30 and any layer of the first and second pluralities of layers may be a layer 30 as shown in FIG. 2 .
  • As shown in FIG. 2 , the layer 30 comprises an inlet 32 and an outlet 34, a sidewall 40, and (with brief reference to FIG. 5 ) an upper sheet 36, and a lower sheet 38. In use, fluid is constrained by the upper sheet 36, lower sheet 38, and sidewall 40, so as to flow from the inlet 32, through the layer 30, to the outlet 34. That is, the upper sheet 36, lower sheet 38, and sidewall 40 together define a flowpath for fluid flowing in the layer 30. The layer 30 shown in FIG. 2 defines a generally U-shaped flowpath between the inlet 32 and outlet 34. The upper sheet 36 of a given layer (e.g. layer 30 b), may simultaneously function as the lower sheet 38 of layer (e.g. layer 30 a) immediately above.
  • With reference to FIG. 1 , a first portion of the first header 12 connects to the inlet side 30 of each layer 30 a,c,e . . . n of the first plurality of layers, and, in use, fluid is pumped into the first portion and flows into the inlet side 32 of every layer connected to the first header 12. The fluid flows through each of the layers 30 a,c,e . . . n and out through the outlet 34 of each layer 30 a,c,e . . . n of the first plurality of layers. The outlets 34 are all connected to a second portion of the first header 12, the second portion being fluidly isolated from the first portion. Fluid flows into the second portion and then out of the first header 12.
  • Similarly, a first portion of the second header 14 connects to the inlet side 30 of each layer 30 b,d . . . n−1 and, in use, fluid is pumped into the first portion and flows into the inlet side 32 of every layer connected to the second header 14. The fluid flows through each of the layers 30 a,c,e, . . . n and out through the outlet 34 of each layer. The outlets 34 are all connected to the second portion of the second header 14, the second portion being fluidly isolated from the first portion. Fluid flows into the second portion and then out of the second header 14.
  • Within each layer 30, as shown in FIG. 2 , one or more pins 100 are disposed in the fluid flowpath. Each pin 100 extends between the lower sheet 38 and the upper sheet 36.
  • Additionally, there may be provided within each layer 30 a first set of turning vanes 42 a that may turn the flow through 90 degrees, and a second set of turning vanes 42 b that may turn the flow through a further 90 degrees, to create the overall U-shaped flow path. A plurality of pins 100 may be disposed between the first and second sets of turning vanes 42 a,b. The pins 100 shown in FIG. 2 are all arranged within the layer 30 such that each pin 100 faces directly into a local flow direction.
  • FIG. 3 shows three sheets 301, 302, 303 (each of which may act as an upper or a lower sheet of a layer 30), each sheet having a different undulating profile. FIG. 4 shows sheets 301, 302, 303 with some exemplary fluid flowpaths that fluid may take when moving across the sheet.
  • Sheet 301 has an undulating profile comprising undulations extending along a first axis X.
  • Sheet 302 has an undulating profile comprising undulations extending along a second axis Y which is non-parallel with the first axis X. In the example shown in FIG. 3 b , the second axis Y is perpendicular to the first axis X, i.e. the second axis Y is oriented at 90 degrees from the first axis X. However, in other examples, the second axis Y may be oriented at any angle between 0 degrees and 180 degrees from the first axis, e.g. at 30 degrees or at 45 degrees. That is, the second axis Y is different from the first axis X, and may be 90 degrees to the first axis X or skew to the first axis X. The first axis X lies in the plane of sheet 301 and the second axis Y lies in the plane of sheet 302.
  • Sheet 303 has an undulating profile comprising undulations extending along the first axis X and undulations extending along the second axis Y. Again, in this example the second axis Y is shown as perpendicular to the first axis X. In other examples, second axis Y may extend at a different angle (i.e. not 90 degrees) to the first axis X. The first axis X and second axis Y lie in the plane of sheet 303.
  • In an example layer 30, sheet 301 forms one of the upper or lower sheet of the layer, and sheet 302 forms the other of the upper or lower sheet of the layer. As the undulating profiles of these sheets are different (in this example, the undulations of each sheet extends along different axes), the flowpath defined between these sheets 301, 302 causes increased turbulence of the fluid flowing through it, and thus increases the mixing of fluid particles. By increasing the turbulence of the flow, the heat transfer coefficient of the layer is increased, thus improving the efficiency of the heat exchanger.
  • In another example, a layer 30 comprises sheet 303 as an upper (or lower) sheet and comprise sheet 301 or sheet 302 as the corresponding lower (or upper) sheet. The undulating profile of sheet 303 comprises an additional set of undulations compared to the undulating profile of sheet 301 or sheet 302 which extends along a different axis (i.e. non-parallel) to the axis of the undulations of sheet 301 or sheet 302, and such an arrangement of sheets thus increases the turbulence of the fluid flowing between. Exemplary fluid paths, which are dictated by the undulating profiles of each of sheet 301, sheet 302, and sheet 303, are shown in FIG. 4 .
  • FIG. 5 shows a side view of a first layer 30 a and a second layer 30 b in the heat exchanger 10. As shown, lower sheet 38 a of the first layer 30 a has an undulating profile comprising undulations extending at least along a first axis X, and upper sheet 36 a of the first layer 30 a also has an undulating profile comprising undulations extending at least along a first axis X. The undulations of each sheet comprise a sequence of alternating peaks and troughs. The undulations may be sinusoidal. The undulations may have a wavelength and a phase. The wavelength of the undulations may be constant, e.g. a distance between each consecutive peak of the undulations is constant.
  • As shown in FIG. 5 , in order to increase turbulence of the fluid flow in the layer 30 a, the undulations of the lower sheet 38 a have a first wavelength w1 that is longer than a second wavelength w2 of the undulations of the upper sheet 36 a. In other words, a first distance between the peaks of the undulations of the lower sheet 38 a may be greater than a second distance between the peaks of the undulations of the upper sheet 36 a.
  • Furthermore, in FIG. 5 , a first phase ϕ1 of the undulations of the lower sheet 38 a is different from a second phase ϕ2 of the undulations of the upper sheet 36 a. In other words, the undulations of the lower sheet 38 a are offset from the undulations of the upper sheet 36 a to promote turbulent flow in the heat exchanger layer 30 a.
  • In the heat exchanger 10, as shown FIG. 5 , the lower sheet 38 a of the first layer 30 a may simultaneously function as an upper sheet 36 b of a second layer 30 b, and in that case the undulating profile of the upper sheet 36 b of layer 30 b is also the undulating profile of the lower sheet 38 a of layer 30 a.
  • The upper sheet 36 a of layer 30 a, which has an undulating profile different to that of the lower sheet 38 a, may have an undulating profile the same as that of the lower sheet 38 b of layer 30 a (e.g. so the undulating profiles of the sheets in the heat exchanger alternate). Alternatively, the undulating profiles of the sheets may be randomly ordered (or ordered in some other manner) provided the undulating profiles of adjacent sheets (i.e. sheets that together form a single layer 30) are different from one another.
  • In FIG. 5 , the undulations of the lower sheet 38 b that are extending along a first axis X have a third wavelength w3 that is different to the first wavelength w1 but the same as the second wavelength w2, and a third phase ϕ3 that is different to the first phase ϕ1 and the second phase ϕ2.
  • As discussed above, the sheets of the first layer 30 a and second layer 30 b may or may not have undulations extending along the second axis Y, but these are not visible in FIG. 5 .
  • The pins 100 in the layer 30 a are arranged in a pin pattern adapted to suit the requirements of the layer 30 a, e.g. considering the undulating profile of the upper sheet 36 a and the undulating profile of the lower sheet 38 a. Each pin 100 extends between the upper and lower sheet, defining a pin height hp. The pin height of each pin is dependent on the positioning of the pins 100 (e.g. the pin pattern) relative to the undulating profiles of the upper sheet and the lower sheet. As such, at least two of the plurality of pins may have different pin heights. For example, a short pin may have a height h p 1 and be positioned at or near to a peak of an undulation of the lower sheet 38 a and connected to the upper sheet 36 at or near to a trough of an undulation of the upper sheet 36 a. A long pin may have a height hp 2 and be positioned at or near to a trough of the lower sheet 38 a so that it may be connected to the upper sheet 36 b at or near a peak of an undulation of the upper sheet 36 a. In this example, the long pin having height hp 2 is longer than the short pin having a height h p 1.
  • The first layer 30 a may have a different number of pins and/or a different pin pattern from the second layer 30 b.
  • Each sheet, not considering the undulating profile, is generally planar in shape, e.g. each sheet generally extends along a plane XY, and the undulations are variations in the “z” direction. In other words, in a generic layer 30, a lower sheet 38 extends along a first plane p1 and an upper sheet 36 extends along a second plane p2. The first plane p1 and the second plane p2 are disposed apart from each other so the upper sheet 36 and lower sheet 38 define the flowpath therebetween. The plane may be defined as the plane that bisects the undulating profile along the direction of undulations of a given sheet.
  • As shown in the example in FIG. 5 , the first plane p1 and the second plane p2 may be parallel (and a third plane p3 of the lower sheet 38 b of the second layer 30 b may also be parallel with the first plane p1 and the second plane p2). In other words, the layer 30 a has a constant average height (note, due to the upper and lower sheets having different undulations e.g. in terms of phase, undulation-direction etc., the height at one point within the layer will differ from the height in another location within that layer). An average height of each layer of the first plurality of layers 30 a,c,e . . . 30 n may be different from an average height of each layer of the second plurality of layers 30 b,d . . . 30 n−1. This may have particular advantages where the first fluid is different from the second fluid.
  • In the example shown in FIG. 6 , the first plane p1 and the second plane p2 are non-parallel. The first plane p1 may be oriented at an angle α between 0 and 10 degrees (e.g. 0°<α≤10°) from the second plane p2 along the X axis, as shown in FIG. 6 . In one example, 5°≤α≤10°. Alternatively or additionally, the first plane p1 and the second plane p2 may be oriented at an angle β between 0 and 10 degrees (e.g. 0°≤β≤10°) from the second plane p2 along the Y axis (not shown). In one example, 5°≤β≤10°. Angling the upper sheet 36 and lower sheet 38 relative to each other may further increase turbulence of the fluid flow in the layer 30.
  • Each sheet may have a first section undulating around the first plane in a first section of the first layer, and may have a second section wherein the undulations undulate around a different plane. That is, the different plane may be non-co-planar with the first plane of the first section.
  • Each layer 30 may be produced by additive manufacturing, such as by the process shown in FIG. 7 . In the method 500, a lower sheet 38 is additively manufactured, the lower sheet 38 having a first undulating profile (step 502). At step 504, pins 100 are additively manufactured on the lower sheet 38. At step 506, an upper sheet 36 is provided on top of the pins 100, the upper sheet 36 having a second undulating profile different from the first undulating profile.
  • The process may optionally include additively manufacturing one or more of: the sidewall 40, turning vanes 42 a,b, further layers 30 on top of the initially formed layer 30, and one or more headers connecting to each layer 30.
  • Each layer 30 may be produced by a SLM powder-bed method of additive manufacturing. In this method, a first layer of metal powder is provided and a portion of the powder is melted by a laser beam to “print” the first layer of the overall object. The first layer is then lowered and a second layer of powder is brushed over the first layer, and a portion of the second layer of powder is melted by the laser beam to print a second layer of the overall object. In this way, a three-dimensional object is built-up layer-by-layer and, once all layers of the object have been printed, the loose (i.e. unmelted) powder is removed to reveal the object.
  • The upper sheet 36 may be a pre-existing (e.g. manufactured by a previous additive manufacturing process) layer that is connected to the top of the pins 100 after construction of the pins 100 on the lower sheet 38. Alternatively, the upper sheet 38 may be additively manufactured after the pins 100 have been manufactured, by continuing the additive manufacturing process.
  • After a first layer 30 (e.g. layer 30 n) of the heat exchanger core 11 is formed, a new layer 30 (e.g. layer 30 n−1) may be formed directly on top of the first layer 30. In this case, the upper sheet 36 of the first layer 30 becomes the bottom sheet 38 of the new layer 30. That is, the same layer of material may simultaneously function as the upper sheet 36 of one layer 30, and the bottom sheet 38 of another layer 30.
  • The sidewall 40 may have an undulating cross-section, e.g. as shown in FIGS. 1 and 2 . This may increase the heat transfer across the sidewall 40 and/or may increase the strength of the sidewall for a given wall thickness.
  • Any or all parts of the heat exchanger 10 may be made from metal. In some embodiments, some or all parts are made from an austenitic nickel-chromium-based superalloy, such as the Iconel family of metals manufactured by the Special Metals Corporation of New York state, USA. In other embodiments, some or all parts may be made from an aluminium alloy or a titanium alloy.
  • The first and second fluids may be oil, such that the heat exchanger 10 is an oil-oil heat exchanger. However, in other embodiments, the first fluid may be different from the second fluid. Other fluids, including air, water, fuel(s), or carbon dioxide are also envisaged for either or both of the first and second fluids.

Claims (16)

What is claimed is:
1. A layer for a heat exchanger, the layer comprising:
an inlet;
an outlet;
an upper sheet;
a lower sheet;
a fluid flowpath defined between the upper sheet and lower sheet and from the inlet to the outlet; and
at least one pin disposed in the flowpath and connecting the upper sheet to the lower sheet;
wherein the lower sheet has a first undulating profile; and
wherein the upper sheet has a second undulating profile different from the first undulating profile.
2. The layer according to claim 1, wherein each undulating profile comprises at least one of:
undulations extending along a first axis; and
undulations extending along a second axis;
wherein the first axis and the second axis are non-parallel.
3. The layer according to claim 2, wherein the first undulating profile comprises undulations extending along the first axis and having a first undulation wavelength, and the second undulating profile comprises undulations extending along the first axis and having a second undulation wavelength different from the first undulation wavelength.
4. The layer according to claim 2, wherein the first undulating profile comprises undulations extending along the first axis and having a first phase of undulation, and the second undulating profile comprises undulations extending along the first axis and having a second phase of undulation different from the first phase of undulation.
5. The layer according to claim 1, wherein the at least one pin comprises a plurality of pins disposed in the flowpath, each pin of the plurality of pins connecting between the upper sheet and lower sheet and having a pin height defined between the upper and lower sheet, wherein at least two of the plurality of pins have different pin heights.
6. The layer according to claim 1, wherein at least one of the upper sheet or the lower sheet are formed from an aluminium alloy, a titanium alloy, or an austenitic nickel-chromium-based superalloy.
7. A heat exchanger comprising a first layer and a second layer, wherein:
the first layer and the second layer are each a layer according to claim 1; and
the upper sheet of the second layer is also the lower sheet of the first layer.
8. The heat exchanger according to claim 7, wherein the upper sheet of the first layer extends along a first plane and the lower sheet of the first layer extends along a second plane, and wherein the first plane and second plane are not parallel.
9. The heat exchanger according to claim 7, wherein the upper sheet of the first layer extends along a first plane and the lower sheet of the first layer extends along a second plane, and wherein the first plane and second plane are parallel.
10. The heat exchanger according to claim 9, wherein the lower sheet of the second layer extends along a third plane, the third plane being parallel with the first plane and the second plane; and wherein a first average height defined between the upper and lower sheets of the first layer is different from a second average height defined between the upper and lower sheets of the second layer.
11. The heat exchanger according to claim 1, wherein the number of pins disposed in the flowpath of the first layer is different from the number of pins disposed in the flowpath of the second layer.
12. A method of additively manufacturing a layer for a heat exchanger, the method comprising:
additively manufacturing a lower sheet having a first undulating profile;
additively manufacturing at least one pin on the lower sheet; and
providing an upper sheet on top of the at least one pin, the upper sheet having a second undulating profile different from the first undulating profile.
13. The method according to claim 12, wherein additively manufacturing at least one pin on the lower sheet comprises additively manufacturing a plurality of pins on the lower sheet, wherein at least two of the plurality of pins have a different pin height.
14. A method of additively manufacturing a heat exchanger, the method comprising:
additively manufacturing a first plurality of layers interleaved with a second plurality of layers, wherein each layer of the first and second pluralities of layers is manufactured via the method of claim 12;
additively manufacturing a first header fluidly connected to each of the first plurality of layers; and
additively manufacturing a second header fluidly connected to each of the second plurality of layers.
15. The method according to claim 12, wherein each step of additive manufacturing is performed using a metal powder bed SLM additive manufacturing process.
16. The method according to claim 15, wherein a powder of the metal powder bed is one of an aluminium alloy, a titanium alloy, or an austenitic nickel-chromium-based superalloy.
US18/059,980 2022-01-08 2022-11-29 Heat exchanger with undulating parting sheets Pending US20230221082A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP22461501.3 2022-01-08
EP22461501.3A EP4209348A1 (en) 2022-01-08 2022-01-08 Heat exchanger with undulating parting sheets

Publications (1)

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US20230221082A1 true US20230221082A1 (en) 2023-07-13

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Application Number Title Priority Date Filing Date
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US (1) US20230221082A1 (en)
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Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3255816A (en) * 1962-01-02 1966-06-14 Rosenblad Corp Plate type heat exchanger
SE7509633L (en) * 1975-02-07 1976-08-09 Terence Peter Nicholson DEVICE FOR FLAT HEAT EXCHANGER
US6019160A (en) * 1998-12-16 2000-02-01 Abb Air Preheater, Inc. Heat transfer element assembly
FR3055951B1 (en) * 2016-09-14 2019-06-14 Commissariat A L'energie Atomique Et Aux Energies Alternatives ENTHALPIC EXCHANGER WITH SIMPLIFIED DESIGN
EP3608617B1 (en) * 2018-08-06 2020-12-16 LEONARDO S.p.A. Heat exchanger for an aircraft
EP3614091B1 (en) * 2018-08-24 2024-04-10 HS Marston Aerospace Limited Hybrid pin-fin-plate heat exchanger

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